JPS62286563A - Cyclone type electrostatic precipitator - Google Patents
Cyclone type electrostatic precipitatorInfo
- Publication number
- JPS62286563A JPS62286563A JP61130288A JP13028886A JPS62286563A JP S62286563 A JPS62286563 A JP S62286563A JP 61130288 A JP61130288 A JP 61130288A JP 13028886 A JP13028886 A JP 13028886A JP S62286563 A JPS62286563 A JP S62286563A
- Authority
- JP
- Japan
- Prior art keywords
- main body
- fine particles
- cyclone main
- cyclone
- medium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000012717 electrostatic precipitator Substances 0.000 title claims description 4
- 239000000428 dust Substances 0.000 claims abstract description 12
- 239000003595 mist Substances 0.000 claims abstract description 6
- 239000003496 welding fume Substances 0.000 claims description 5
- 239000010419 fine particle Substances 0.000 abstract description 21
- 230000005611 electricity Effects 0.000 abstract description 6
- 239000011362 coarse particle Substances 0.000 abstract description 4
- 230000016615 flocculation Effects 0.000 abstract 1
- 238000005189 flocculation Methods 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 238000011084 recovery Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 239000012212 insulator Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 239000008162 cooking oil Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
- B03C3/15—Centrifugal forces
Abstract
Description
【発明の詳細な説明】
3、発明の詳細な説明
[産業上の利用分野]
本発明は溶接ヒユーム、オイルミストの如き媒体内に含
有される微粒子等を集塵除去するに好適なサイクロン式
電気集塵装置に関するものである。Detailed Description of the Invention 3. Detailed Description of the Invention [Industrial Application Field] The present invention is a cyclone-type electric motor suitable for collecting and removing fine particles contained in media such as welding fumes and oil mist. This relates to a dust collector.
[従来の技術]
溶接ヒユーム、オイルミストの如き媒体内の微粒子、粉
末(微粒子等)を集塵除去する装置としては、?tF電
された適宜メツシュのネット部材およびこれに対峙して
配設される電極間に前記媒体を導入し、前記微粒子等を
静電凝縮しながら粗大化し、これを前記ネット部材に吸
着せしめて除去するものが一般に採用されていた。[Prior Art] What is a device for collecting and removing fine particles and powder (fine particles, etc.) in media such as welding fumes and oil mist? The medium is introduced between an appropriate mesh net member subjected to tF electricity and an electrode disposed opposite to the medium, and the fine particles, etc. are electrostatically condensed and coarsened, and the particles are adsorbed to the net member and removed. Those that did were generally adopted.
[発明が解決しようとする問題点]
従来技術では前記の如くネット部材に微粒子等が吸着す
るが、該微粒子等が粘着性に富む場合にはこれをネット
部材から除去することが困難となり、クリーニング性に
劣る問題点が生ずる。またネット部材の間隙から微粒子
等が通り抜け、除去率が低下する欠点が生ずる。[Problems to be Solved by the Invention] In the prior art, fine particles etc. are adsorbed to the net member as described above, but if the fine particles etc. are sticky, it is difficult to remove them from the net member, and cleaning is difficult. Problems that are inferior to gender arise. Further, there is a drawback that fine particles and the like pass through the gaps in the net member, resulting in a reduction in the removal rate.
本発明は以上の問題点および欠点等を解決するもので微
粒子等を有効に分離すると共にこの回収量を増大し、除
去率を向上するサイクロン式電気集塵装置を提供するこ
とにある。The present invention solves the above-mentioned problems and drawbacks, and aims to provide a cyclone electrostatic precipitator that can effectively separate fine particles, increase the amount of collected particles, and improve the removal rate.
[問題点を解決するための手段] 本発明はこのために流入された溶接ヒユーム。[Means for solving problems] The present invention is a welding fume introduced for this purpose.
オイルミストの如き媒体を旋回して排出すると共に高圧
加電された壁部を有するサイクロンと、該サイクロン内
の前記媒体と接する位置に配設され高圧加電される放電
極とを設けてなるサイクロン式電気集塵装置を構成する
ものである。A cyclone that swirls and discharges a medium such as oil mist and has a wall portion that is electrified with high voltage, and a discharge electrode that is placed in contact with the medium within the cyclone and is energized with high voltage. This constitutes a type electrostatic precipitator.
[作 用]
流入された媒体をサイクロン内で旋回させながら通過さ
せ、含有する微粒子等を静電凝縮し、これを前記放電極
により順次粗大化して前記サイクロンの壁部に吸着せし
め、これを適宜位置に集約せしめて除去する。[Function] The inflowing medium is passed through the cyclone while being swirled, and the contained fine particles are electrostatically condensed, and the particles are gradually coarsened by the discharge electrode and adsorbed to the wall of the cyclone, and are then appropriately removed. Concentrate it in one location and remove it.
[実施例] 以下1本発明の実施例を図面に基づき説明する。[Example] An embodiment of the present invention will be described below based on the drawings.
第1図に示す如く、サイクロン1は円筒状サイクロン本
体2と該サイクロン本体2に偏心して配設される排風管
3および案内板4等とから形成される。ファン5に連結
する連結管6はサイクロン本体2の外周接線方向(第2
図に示す)に沿って連結される。以上の構造により7ア
ン5の吸引ロアから吸引された溶接ヒユーム、オイルミ
ストの如き媒体は連結管6からサイクロン本体2内流入
され気流旋回しながら図の下方側に送られる。なお案内
板4は前記媒体の通過効率を向上せしめる効果を有する
が必ずしも配設する必要はない。サイクロン本体2図の
下方側には集塵室8が設けられ、集塵室8内には集塵さ
れた微粒子等の集塵状態を点検すると共にこれを排出す
るための点検排出口9およびこのカバ10が設けられて
いる。なおりバlOにはドレン抜き11が設けられる。As shown in FIG. 1, the cyclone 1 is formed from a cylindrical cyclone body 2, an exhaust pipe 3, a guide plate 4, etc., which are eccentrically arranged on the cyclone body 2. The connecting pipe 6 connected to the fan 5 is connected in the tangential direction of the outer circumference of the cyclone main body 2 (second
(as shown in the figure). With the above structure, media such as welding fume and oil mist sucked from the suction lower of the 7-an 5 flow into the cyclone body 2 through the connecting pipe 6 and are sent to the lower side in the figure while swirling the airflow. Note that although the guide plate 4 has the effect of improving the passage efficiency of the medium, it is not necessarily necessary to provide it. A dust collection chamber 8 is provided on the lower side of the cyclone body 2, and inside the dust collection chamber 8 there is an inspection outlet 9 for inspecting the state of collected fine particles, etc. and for discharging them. A cover 10 is provided. A drain 11 is provided in the opening bar 1O.
サイクロン本体2の図の上方側には針端放電極12が設
けられている。針端放電極12の電極部12Aはサイク
ロン本体2内に膨出して配設され、サイクロン本体2内
に流入される前記媒体に接する。A needle end discharge electrode 12 is provided on the upper side of the cyclone body 2 in the figure. The electrode portion 12A of the needle end discharge electrode 12 is disposed in a bulged manner within the cyclone body 2, and comes into contact with the medium flowing into the cyclone body 2.
また第2図に示す如く針端放電極12は複数個(図示で
は3個)配設されると共に、サイクロン本体2とは絶縁
物13により絶縁されて固定される。Further, as shown in FIG. 2, a plurality of needle end discharge electrodes 12 (three in the figure) are provided, and are insulated and fixed from the cyclone body 2 by an insulator 13.
高圧電源部14に連結する電線15. teはサイクロ
ン本体2の壁部と針端放電極12にそれぞれ連結し、相
互にプラス又はマイナスの高圧直流電気(1万ポルト以
上)を加電している。Electric wire 15 connected to high voltage power supply section 14. te is connected to the wall of the cyclone body 2 and the needle end discharge electrode 12, respectively, and applies positive or negative high voltage DC electricity (10,000 ports or more) to each other.
第3図に示す如く、集塵室8内にはカバlO側に向って
下降傾斜する傾斜板17が設けられ、集塵室8内の前記
微粒子等をカバIO側に送り込むようにしている。これ
により微粒子等の排出性を向上することができる。また
集塵室形状としては第4図に示す如くサイクロン本体2
の下方側をテーパに形成され、これに開閉弁18を設置
した集塵室8Aを用いてもよい。As shown in FIG. 3, an inclined plate 17 that slopes downward toward the cover IO side is provided in the dust collection chamber 8 to send the fine particles and the like in the dust collection chamber 8 to the cover IO side. This improves the ability to discharge fine particles and the like. The shape of the dust collection chamber is as shown in Figure 4.
A dust collection chamber 8A having a tapered lower side and an on-off valve 18 installed therein may be used.
次に、本実施例の作用を更に詳しく説明する。Next, the operation of this embodiment will be explained in more detail.
ファン5の吸引ロアから吸引された前記媒体は連結管6
からサイクロン本体2内に流入され、サイクロン本体2
内を気流旋回し下方に送られなから排風v3から排風さ
れる。前記媒体内に含有される微粒子等はサイクロン本
体内を通過する際に針端放電極12の電極部12Aに接
すると共に針端放電極12とサイクロン本体2の前記壁
部間のプラスおよびマイナスの高圧直流電気加電によっ
て発生する強力なコロナ放電による電界内を通過し、こ
の際に静電凝縮され、前記気流旋回による遠心運動によ
り静電凝縮を順次増進しながら粗大化する。粗大化した
粗粒子群はサイクロン本体2の前記壁部に電気的に吸着
する。前記壁部に吸着した粗粒子群は集塵室8(8A)
側に送られ、堆積して回収される。微粒子等を除去され
た媒体は前記の如く排風管3より排出される。なお第3
図に示す傾斜板17上に堆積した前記微粒子等は傾斜下
方端のカバ10側に送られ容易に排出除去される。The medium sucked from the suction lower of the fan 5 is transferred to the connecting pipe 6
Flows into the cyclone body 2 from the cyclone body 2.
The airflow is not sent downward by swirling inside the air, but is exhausted from the exhaust air v3. When the fine particles contained in the medium pass through the cyclone body, they come into contact with the electrode portion 12A of the needle end discharge electrode 12, and the positive and negative high pressures between the needle end discharge electrode 12 and the wall portion of the cyclone body 2 are generated. It passes through an electric field due to a strong corona discharge generated by DC electric current application, and is electrostatically condensed at this time, and becomes coarser as the electrostatic condensation is gradually increased due to the centrifugal movement caused by the swirling of the airflow. The coarse particles are electrically attracted to the wall of the cyclone body 2. The coarse particles adsorbed on the wall are collected in the dust collection chamber 8 (8A).
It is sent to the side, deposited and collected. The medium from which fine particles and the like have been removed is discharged from the exhaust pipe 3 as described above. Furthermore, the third
The fine particles and the like deposited on the inclined plate 17 shown in the figure are sent to the cover 10 side at the lower inclined end and are easily discharged and removed.
tjSZ図に示す如き3個の針端放電極12を採用した
本実施例の実験例として風量的20m3/winで外周
筒直径400m1nのサイクロン本体2内に微粒子等を
流入した場合、次の如きデータが得られた。すなわちサ
イクロン本体2および針端放電極12を高圧加電した場
合には、投入された粒径モ均20色の粉末410gの内
400gのものが回収された。すなわち97.58%の
回収効率が上げられた。また加電しない場合は400g
の投置に対し355gの回収量があり。As an experimental example of this embodiment employing three needle end discharge electrodes 12 as shown in the tjSZ diagram, when fine particles, etc. are flowed into the cyclone body 2 with an air volume of 20 m3/win and an outer cylinder diameter of 400 m1n, the following data are obtained. was gotten. That is, when high voltage was applied to the cyclone body 2 and the needle end discharge electrode 12, 400 g of the 410 g of powder of 20 colors of uniform particle size put in was recovered. In other words, the recovery efficiency was increased to 97.58%. Also, if no electricity is applied, 400g
There was a recovery amount of 355g for the 355g deposited.
回収効率88.75%となった。また食用油を沸唱させ
排風管3の排風口にガーゼを吊るし、油による色の変化
を調べる実験においては、前記加電のものは加電したも
のに較べ、同一色度に達するに約4.9倍だけ多くの時
間を要することがわかった。The recovery efficiency was 88.75%. In addition, in an experiment in which cooking oil was boiled and gauze was hung from the exhaust port of the exhaust pipe 3 to examine the change in color caused by the oil, it was found that the energized version reached the same chromaticity compared to the electrified version. It turns out that it takes 4.9 times more time.
更にこの場合加電しないとき目視可能の油煙が加電した
場合には目視し得ないことも明らかになった。Furthermore, it has become clear that in this case, oil smoke that is visible when no electricity is applied is not visible when electricity is applied.
以上の如く、本実施例の如く高圧加電したものは大きな
微粒子回収効率を上げることがわかった。As described above, it was found that applying high voltage as in this example greatly increases the particle collection efficiency.
本実施例において第1図の2点鎖線に示す如く、排風管
3の排風口を覆う消音ボックス19、これに設けられた
フィルタ状排風口20および装置全体を円滑に移動させ
るキャスタ21等を付設せしめるようにしてもよい。In this embodiment, as shown by the two-dot chain line in FIG. 1, a noise reduction box 19 that covers the exhaust port of the exhaust pipe 3, a filter-like exhaust port 20 provided therein, casters 21 for smoothly moving the entire device, etc. are installed. It may be made to be attached.
以上の説明によって明らかな如く2本発明によれば微粒
子等を有効に分離し、この回収量を増大し、除去率を向
上し得る効果が上げせられる。As is clear from the above description, according to the present invention, it is possible to effectively separate fine particles, increase the amount of collected particles, and improve the removal rate.
第1図は本発明の全体構造図、第2図は第1図における
針端放電極およびサイクロン本体構造を示す上面図、第
3図および第4図は実施例の集塵室内の構造を示す一部
断面図である。
l・・・サイクロン、?・・・サイクロン本体、3・・
・排風管、4・・・案内板、5・・・ファン。
6・・・連結管、7・・・吸引口、8.8A・・・集塵
室、9・・・点検排出口、10・・・カバ、11・・・
ドレン抜き、12・・・針端放電極、12A・・・電極
部、13・・・絶縁物、14・・・高圧?!源部、 1
5.18・・・電線、17・・・傾斜板、1B・・・開
閉弁、19・・・消音ボックス、20・・・フィルタ状
排風口、2I・・・キャスタ。Fig. 1 is an overall structural diagram of the present invention, Fig. 2 is a top view showing the needle end discharge electrode and cyclone main body structure in Fig. 1, and Figs. 3 and 4 show the structure inside the dust collection chamber of the embodiment. It is a partially sectional view. l...Cyclone? ...Cyclone body, 3...
・Exhaust pipe, 4... Information board, 5... Fan. 6... Connecting pipe, 7... Suction port, 8.8A... Dust collection chamber, 9... Inspection outlet, 10... Cover, 11...
Drain drain, 12...needle end discharge electrode, 12A...electrode part, 13...insulator, 14...high voltage? ! Genbu, 1
5.18... Electric wire, 17... Inclined plate, 1B... Open/close valve, 19... Silence box, 20... Filter-like exhaust port, 2I... Caster.
Claims (1)
塵して除去する集塵装置において、流入された前記媒体
を気流旋回して排出すると共に高圧加電された壁部を有
するサイクロンと、該サイクロン内の前記媒体と接する
位置に配設され高圧加電される放電極とを設けることを
特徴とするサイクロン式電気集塵装置。A dust collector for collecting and removing particulates in a medium such as welding fume and oil mist, which includes a cyclone that discharges the inflowing medium by swirling the medium and has a wall section that is electrified with high voltage; A cyclone type electrostatic precipitator, characterized in that a discharge electrode is provided in a position in contact with the medium and is applied with a high voltage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61130288A JPS62286563A (en) | 1986-06-06 | 1986-06-06 | Cyclone type electrostatic precipitator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61130288A JPS62286563A (en) | 1986-06-06 | 1986-06-06 | Cyclone type electrostatic precipitator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62286563A true JPS62286563A (en) | 1987-12-12 |
Family
ID=15030733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61130288A Pending JPS62286563A (en) | 1986-06-06 | 1986-06-06 | Cyclone type electrostatic precipitator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62286563A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003001411A (en) * | 2001-06-21 | 2003-01-08 | Matsushita Electric Ind Co Ltd | Method and device for removing flux |
CN101804383A (en) * | 2010-03-25 | 2010-08-18 | 江苏力洁达环保设备工程有限公司 | Differential electric precipitator |
CN107110519A (en) * | 2015-06-24 | 2017-08-29 | Lg电子株式会社 | Air purifier |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4842179B1 (en) * | 1969-10-25 | 1973-12-11 | ||
JPS5398577A (en) * | 1977-02-09 | 1978-08-29 | Ishikawajima Harima Heavy Ind Co Ltd | Electric centrifugal dust collector |
JPS5745356A (en) * | 1980-09-02 | 1982-03-15 | Fuji Electric Co Ltd | Dust collector |
-
1986
- 1986-06-06 JP JP61130288A patent/JPS62286563A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4842179B1 (en) * | 1969-10-25 | 1973-12-11 | ||
JPS5398577A (en) * | 1977-02-09 | 1978-08-29 | Ishikawajima Harima Heavy Ind Co Ltd | Electric centrifugal dust collector |
JPS5745356A (en) * | 1980-09-02 | 1982-03-15 | Fuji Electric Co Ltd | Dust collector |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003001411A (en) * | 2001-06-21 | 2003-01-08 | Matsushita Electric Ind Co Ltd | Method and device for removing flux |
JP4580590B2 (en) * | 2001-06-21 | 2010-11-17 | パナソニック株式会社 | Flux removal method and apparatus |
CN101804383A (en) * | 2010-03-25 | 2010-08-18 | 江苏力洁达环保设备工程有限公司 | Differential electric precipitator |
CN107110519A (en) * | 2015-06-24 | 2017-08-29 | Lg电子株式会社 | Air purifier |
CN107110519B (en) * | 2015-06-24 | 2021-01-12 | Lg电子株式会社 | Air purifier |
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